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WO1985000501A1 - A process for making portioned cheese - Google Patents

A process for making portioned cheese Download PDF

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Publication number
WO1985000501A1
WO1985000501A1 PCT/DK1984/000071 DK8400071W WO8500501A1 WO 1985000501 A1 WO1985000501 A1 WO 1985000501A1 DK 8400071 W DK8400071 W DK 8400071W WO 8500501 A1 WO8500501 A1 WO 8500501A1
Authority
WO
WIPO (PCT)
Prior art keywords
acidogen
milk
cheese
additives
cheese milk
Prior art date
Application number
PCT/DK1984/000071
Other languages
French (fr)
Inventor
Jens Peter Syppli Hansen
Original Assignee
Jens Peter Hansen, Aarhus A/S
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Jens Peter Hansen, Aarhus A/S filed Critical Jens Peter Hansen, Aarhus A/S
Priority to UA3882451A priority Critical patent/UA5549A1/en
Priority to DE8484902915T priority patent/DE3475259D1/en
Priority to AT84902915T priority patent/ATE38761T1/en
Publication of WO1985000501A1 publication Critical patent/WO1985000501A1/en
Priority to FI851232A priority patent/FI82880C/en
Priority to LV930966A priority patent/LV5363A3/en
Priority to MD94-0144A priority patent/MD100C2/en

Links

Classifications

    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING OR TREATMENT THEREOF
    • A23C19/00—Cheese; Cheese preparations; Making thereof
    • A23C19/02—Making cheese curd
    • A23C19/028—Making cheese curd without substantial whey separation from coagulated milk
    • A23C19/0285—Making cheese curd without substantial whey separation from coagulated milk by dialysis or ultrafiltration
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING OR TREATMENT THEREOF
    • A23C19/00—Cheese; Cheese preparations; Making thereof
    • A23C19/02—Making cheese curd
    • A23C19/028—Making cheese curd without substantial whey separation from coagulated milk

Definitions

  • the present invention relates to a process for making portioned cheese, in particular fresh unripe cheeses, such as White Cheese, Feta, Cream Cheese, Cheddar and cottage cheese.
  • the starting material is usually cow's milk or goat's milk, which may be homogenized.
  • the milk may be used as whole milk, i.e. with its total solids content, or a major or minor portion of the cream may be centri- fuged off.
  • the milk is coagulated by addition of rennet, and the coagulum is processed into cheese in several processing steps, comprising filtration of the separated whey, pressing in moulds and ripening or storage of the pressed cheeses. Sometimes the coagulum is also cooked and washed.
  • rennet instead of coagulating the milk by addition of rennet it is known to effect acidification, either by addition of a lactic acid forming bacterial culture or an inorganic acid, such as phosphoric acid, or an organic acid, e.g. lactic acid or gluconic acid. Also a neutral acidogen may be added, such as glucono-delta-lactone which releases gluconic acid by hydrolysis, cf. the US Patent Specifications 2 982 654 and 3 620 768.
  • OMP W1P which about 3.5? ⁇ is protein, about 3.5.0 is fat and the balance is lactose, minerals and small amounts of other substances, such as vitamins, etc.
  • Ultrafiltration causes removal of a large portion of the water and the low-molecular substances, in particular the lactose and minerals, dissolved in the water.
  • the retentate with a concentration of 35 to 40? ⁇ solids constitutes a liquid cheese milk, which is processed into cheese in the usual manner by coagulation of the protein, recovery of the coagulum, pressing and subsequent treatment in the usual manner .
  • the described method of making cheese is very time- consuming and laborious. It is moreover uneconomical in that a considerable portion of the solids of the milk is lost, e.g. by low fermentation processes, or occurs in by-products of low commercial value.
  • the object of the present invention is to provide a more rational and labour-saving process for making portioned cheese .
  • Another object of the invention is to make cheeses with an improved yield, i.e. with a greater content of the original solids content of the milk.
  • the invention relates to a process for making portioned cheese, wherein concentrated cheese milk is mixed, preferably continuously, with ordinary auxiliary substances and additives, including acidogen, for starting the curdling and ripening processes, and then the mixture is filled into individual packages which are closed hermetically and left to- stand at a suitable temperature until the curdling and ripening processes are completed, and the process is characterized by using a chemically well-defined acidogen, adapting the amount of the acidogen and the mixing conditions, including temperatures and flow periods, etc., so that the concentrated cheese milk containing the said auxiliary substances and additives coagulate preferably after the introduction into the individual packages and is trans ⁇ formed through the curdling and ripening processes.
  • the making of cheese by the process of the invention is preferably continuous, as mentioned, there being used concentrated cheese milk, which has got the composition the finished cheese is to have by addition of common auxiliary substances and additives, such as rennet, lipase, organic acids, calcium chloride, stabilizers, emulsifiers , phosphates, citrates, salts and acidogens. While liquid, the mixture is distributed in small containers, which are closed hermetically and stored under conditions which, because of the presence of acidogen, result in coagulation and cheese formation and also ripening.
  • common auxiliary substances and additives such as rennet, lipase, organic acids, calcium chloride, stabilizers, emulsifiers , phosphates, citrates, salts and acidogens.
  • the cheese milk containing auxiliary substances and additives is expediently pumped through a closed pipe system in which the mixing with acidogen takes place and from where the mixture is dis ⁇ claimedd directly into the indivicual packages.
  • the process can be controlled with great accuracy.
  • temperatures and treatment periods can be adjusted more favourably so that no coagulation or only partial co ⁇ agulation will take place before the mixture has been transferred to the individual packages.
  • the fer- mentation reactions and ripening processes characteristic of the cheese formation preferably take place in the package after it has been closed hermetically.
  • the method is very labour-saving and can be carried out without any risk of contamination. It is not necessary to add bacterial cultures, which do not have a well- defined composition and whose effect is difficult to control.
  • the use of a chemically well-defined acidogen permits a precise pH adjustment to be maintained so that the curdling and ripening processes proceed uniformly and at a constant rate during the continuous process.
  • the preferred acidogen is glucono-delta-lactone, but it is also possible to use another chemical compound with corresponding properties, such as those described in the US Patent Specification 3 620 768.
  • the finished cheese product has retained the original composition of the milk solids essentially unchanged. There is no conversion of the lactose contained in the milk. The yield is therefore high in relation to milk solids.
  • the cheese milk used as the starting material is ex ⁇ pediently formed by ultrafiltration or diafiltration which gives a liquid concentrate with a high content of protein .
  • the additives including the acidogen, are expediently introduced continuously by metering means in the pipe system for mixing with the cheese milk.
  • the acidogen can be introduced in the concentrated cheese milk in the form of a dry powder by means of a screw or a worm metering device, from which the atmospheric air has been expelled by means of gaseous carbon dioxide. This obviates the necessity of suspending or dissolving the acidogen in water with consequent dilution of the cheese milk and of introducing air into the cheese, which might cause bubbles or holes.
  • Milk with a pH of 6.7 and about 12? ⁇ solids, about 3.4? ⁇ protein and about 3.5? ⁇ fat is heated to 98°C for 15 seconds. Then it is cooled to 60°C and homogenized at a pressure of 190 kg/cm 2 , cooled to 8°C and mixed with an 0.15? ⁇ starter distillate through a static in-line mixer for immediate reduction of pH to 6.10.
  • the mixture is allowed to rest for 0.5 to 8 hours.
  • the retentate is mixed with an ⁇ . 1% emulsifier stabilizer and is homogenized at 60 kg/cm 2 and heated to 98°C for 15 seconds and cooled to 28°C.
  • the mixture in liquid shape is immediately dispensed into individual plastics cups or other individual packages.
  • the package is sealed hermetically and left to stand at room temperature until the cheese has developed into a cuttable or spreadable type by renneting, acidification, coagulation and ripening.
  • Milk with a pH of 6.7, about 12? ⁇ solids, about 3.4? ⁇ protein and about 3.5? ⁇ fat is mixed with 13? ⁇ butter and/or vegetable fat and 13. ⁇ caseinate, is heated to 98°C for 15 seconds, cooled to 60°C and homogenized at a pressure of 190 kg/cm 2 and cooled to 12°C, and 0.25? ⁇ organic nutritional acid is added through a static in-line mixer for immediate reduction of pH to 5.20.
  • the mixture is allowed to rest for 0.5 to 8 hours.
  • the acidified concentrate is heated to 31°C.
  • OMP ater and 1 part of salt are added to the concentrate throug a static in-line mixer.
  • the mixture is immediately dispensed in a liquid or partially coagulated form into plastics cups or other packages and is closed hermetically.
  • the packaged product is left to stand until renneting, acidification, coagulation and ripening of the cheese is completed in the package.
  • Example 1 is repeated w th the change that the starting material is reconstituted milk, made of 12 parts of milk solids which are dissolved in 88 parts of water and emulsified together with 13. ⁇ butter, based on the weight of the finished mixture. This gives a spreadable cream cheese .
  • Example 1 is repeated with the change that the additives i.e. rennet, citrate, glucono-delta-lacto ⁇ e and salt, are mixed in a dry state and introduced into the pipe system for mixing with the cheese milk by means of a worm metering device, from which the atmospheric air has been removed by flushing with gaseous carbon dioxide,
  • the additives i.e. rennet, citrate, glucono-delta-lacto ⁇ e and salt
  • the cheese product obtained is of the same type as a co tage cheese .
  • Milk with a pH of about 6.5- and about 12% solids, about 3.4? ⁇ protein and about 3.5? ⁇ fat is heated to about 98°C for 15 seconds. Then it is cooled to about 60°C and homogenized at a pressure of about 190 kg/cm 2 , cooled to about 55°C and ultrafiltrated to provide a retentate with about 38? ⁇ solids.
  • the retentate is homogenized at about 60 kg/cm 2 and is heated to 90°C for about 15 seconds and cooled to about 28°C.
  • Salt in a dry state is mixed with the retentate, and 40 parts of water, 1/2 part of rennet and 20 parts of glucono-delta-lactone are added to the retentate.
  • the mixture is immediately dispensed in a liquid form into individual packages which are closed hermetically.
  • the packaged product is left to stand until renneting, acidification and coagulation is completed, and is then left for curing at about 5°C.
  • the produced cheese is of the Feta type and has the composition:

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  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Polymers & Plastics (AREA)
  • Dairy Products (AREA)

Abstract

A process for making portioned cheese, wherein concentrated cheese milk is continuously mixed with ordinary auxiliary substances and additives, including a well-defined acidogen, for starting the curdling and ripening processes, and is then filled into suitable individual packages which are closed hermetically, is carried out under such controlled conditions that the mixed product is liquid when it is filled into the package, and that the product then coagulates in the package and undergoes the curdling and ripening processes when left to stand at a suitable temperature. The manufacturing process gives a high yield of uniform products and reduces the costs owing to the labour-saving, rational and continuous operation.

Description

A process for making portioned cheese
The present invention relates to a process for making portioned cheese, in particular fresh unripe cheeses, such as White Cheese, Feta, Cream Cheese, Cheddar and cottage cheese.
When cheese is manufactured according to the classic method the starting material is usually cow's milk or goat's milk, which may be homogenized. The milk may be used as whole milk, i.e. with its total solids content, or a major or minor portion of the cream may be centri- fuged off.
The milk is coagulated by addition of rennet, and the coagulum is processed into cheese in several processing steps, comprising filtration of the separated whey, pressing in moulds and ripening or storage of the pressed cheeses. Sometimes the coagulum is also cooked and washed.
Instead of coagulating the milk by addition of rennet it is known to effect acidification, either by addition of a lactic acid forming bacterial culture or an inorganic acid, such as phosphoric acid, or an organic acid, e.g. lactic acid or gluconic acid. Also a neutral acidogen may be added, such as glucono-delta-lactone which releases gluconic acid by hydrolysis, cf. the US Patent Specifications 2 982 654 and 3 620 768.
Addition of acid to a pH below about 5.0 usually causes instantaneous coagulation of the proteins in the milk.
It is known to replace the whole milk or skim milk starting material in the cheese making by a milk concen¬ trate formed by ultrafiltration or diafiltration of the milk. Whole milk has a solids content of about 12%, of
OMP W1P which about 3.5?ό is protein, about 3.5.0 is fat and the balance is lactose, minerals and small amounts of other substances, such as vitamins, etc. Ultrafiltration causes removal of a large portion of the water and the low-molecular substances, in particular the lactose and minerals, dissolved in the water. The retentate with a concentration of 35 to 40?ό solids constitutes a liquid cheese milk, which is processed into cheese in the usual manner by coagulation of the protein, recovery of the coagulum, pressing and subsequent treatment in the usual manner .
The described method of making cheese is very time- consuming and laborious. It is moreover uneconomical in that a considerable portion of the solids of the milk is lost, e.g. by low fermentation processes, or occurs in by-products of low commercial value.
The object of the present invention is to provide a more rational and labour-saving process for making portioned cheese .
Another object of the invention is to make cheeses with an improved yield, i.e. with a greater content of the original solids content of the milk.
Accordingly, the invention relates to a process for making portioned cheese, wherein concentrated cheese milk is mixed, preferably continuously, with ordinary auxiliary substances and additives, including acidogen, for starting the curdling and ripening processes, and then the mixture is filled into individual packages which are closed hermetically and left to- stand at a suitable temperature until the curdling and ripening processes are completed, and the process is characterized by using a chemically well-defined acidogen, adapting the amount of the acidogen and the mixing conditions, including temperatures and flow periods, etc., so that the concentrated cheese milk containing the said auxiliary substances and additives coagulate preferably after the introduction into the individual packages and is trans¬ formed through the curdling and ripening processes.
The making of cheese by the process of the invention is preferably continuous, as mentioned, there being used concentrated cheese milk, which has got the composition the finished cheese is to have by addition of common auxiliary substances and additives, such as rennet, lipase, organic acids, calcium chloride, stabilizers, emulsifiers , phosphates, citrates, salts and acidogens. While liquid, the mixture is distributed in small containers, which are closed hermetically and stored under conditions which, because of the presence of acidogen, result in coagulation and cheese formation and also ripening. However, it is possible to mix the con¬ centrated cheese milk with the auxiliary substances and the additives portionwise, but the amount of the acidogen and the conditions of mixing are then to be so adapted that the mixture is liquid, non-coagulated or only partly coagulated when it is distributed in the individual packages .
The DE 27 34 825 and the French Patent Specification
2 360 258 disclose a continuous process for making cheese, wherein a concentrated cheese milk is first produced, containing the usual auxiliary substances and additives and having the same composition as the finished cheese is to have. To convert this liquid product to cheese, a particularly adapted acid-forming bacterial culture is added immediately after the liquid product is pasteurized and while it is still hot, viz. 55 to 60°C, and the product is then transferred to a container which is closed hermetically and left to stand under suitable conditions for cheese formation and ripening. However, in this known method it is difficult to control the process and to obtain uniform end products because bacterial cultures often have a varying composition and activity, and because the mixing has to take place at a high temperature involving a risk of uncontrollable deterioration of the bacterial culture.
In the process of the invention, the cheese milk containing auxiliary substances and additives is expediently pumped through a closed pipe system in which the mixing with acidogen takes place and from where the mixture is dis¬ pensed directly into the indivicual packages.
As all additives have a well-defined composition, the process can be controlled with great accuracy. Thus, temperatures and treatment periods can be adjusted more favourably so that no coagulation or only partial co¬ agulation will take place before the mixture has been transferred to the individual packages. Also the fer- mentation reactions and ripening processes characteristic of the cheese formation preferably take place in the package after it has been closed hermetically.
The method is very labour-saving and can be carried out without any risk of contamination. It is not necessary to add bacterial cultures, which do not have a well- defined composition and whose effect is difficult to control. The use of a chemically well-defined acidogen permits a precise pH adjustment to be maintained so that the curdling and ripening processes proceed uniformly and at a constant rate during the continuous process.
The preferred acidogen is glucono-delta-lactone, but it is also possible to use another chemical compound with corresponding properties, such as those described in the US Patent Specification 3 620 768.
-BURE OMPI The finished cheese product has retained the original composition of the milk solids essentially unchanged. There is no conversion of the lactose contained in the milk. The yield is therefore high in relation to milk solids.
The cheese milk used as the starting material is ex¬ pediently formed by ultrafiltration or diafiltration which gives a liquid concentrate with a high content of protein .
The additives, including the acidogen, are expediently introduced continuously by metering means in the pipe system for mixing with the cheese milk. Thus, the acidogen can be introduced in the concentrated cheese milk in the form of a dry powder by means of a screw or a worm metering device, from which the atmospheric air has been expelled by means of gaseous carbon dioxide. This obviates the necessity of suspending or dissolving the acidogen in water with consequent dilution of the cheese milk and of introducing air into the cheese, which might cause bubbles or holes.
The process of the invention ill be explained more fully below by means of some working examples.
EXAMPLE 1
Milk with a pH of 6.7 and about 12?ό solids, about 3.4?ό protein and about 3.5?ό fat is heated to 98°C for 15 seconds. Then it is cooled to 60°C and homogenized at a pressure of 190 kg/cm2, cooled to 8°C and mixed with an 0.15?ό starter distillate through a static in-line mixer for immediate reduction of pH to 6.10.
The mixture is allowed to rest for 0.5 to 8 hours.
IfϋK
O ■ « _. W1P
^ KA The acidified milk is heated to 51°C and ultrafiltrated to provide a retentate with 38?ό solids.
The retentate is mixed with an ϋ . 1% emulsifier stabilizer and is homogenized at 60 kg/cm2 and heated to 98°C for 15 seconds and cooled to 28°C.
An 0.1?ό cold water mixture containing 40 parts of water, 1/2 part of rennet and 1/2 part of citrate (1:40), a ?ό cold water mixture containing 1 part of water, 1 part of glucono-delta-lactone (1:1) and a 7?ό hot water mixture with 1 part of water, 1 part of salt (1:1) are added to the retentate in a static in-line mixer.
The mixture in liquid shape is immediately dispensed into individual plastics cups or other individual packages. The package is sealed hermetically and left to stand at room temperature until the cheese has developed into a cuttable or spreadable type by renneting, acidification, coagulation and ripening.
EXAMPLE 2
Milk with a pH of 6.7, about 12?ό solids, about 3.4?ό protein and about 3.5?ό fat is mixed with 13?ό butter and/or vegetable fat and 13.ό caseinate, is heated to 98°C for 15 seconds, cooled to 60°C and homogenized at a pressure of 190 kg/cm2 and cooled to 12°C, and 0.25?ά organic nutritional acid is added through a static in-line mixer for immediate reduction of pH to 5.20.
The mixture is allowed to rest for 0.5 to 8 hours. The acidified concentrate is heated to 31°C. A 4?ό cold water mixture containing 1 part of water, 1 part of glucono- delta-lactone, an 0.1?ά cold water mixture containing 40 parts of water, 1/2 part of rennet and 1/2 part of lipase and a 3?ό cold water mixture containing 1 part of
OMP ater and 1 part of salt are added to the concentrate throug a static in-line mixer.
The mixture is immediately dispensed in a liquid or partially coagulated form into plastics cups or other packages and is closed hermetically. The packaged product is left to stand until renneting, acidification, coagulation and ripening of the cheese is completed in the package.
EXAMPLE 3
Example 1 is repeated w th the change that the starting material is reconstituted milk, made of 12 parts of milk solids which are dissolved in 88 parts of water and emulsified together with 13.ό butter, based on the weight of the finished mixture. This gives a spreadable cream cheese .
EXAMPLE 4
Example 1 is repeated with the change that the additives i.e. rennet, citrate, glucono-delta-lactoπe and salt, are mixed in a dry state and introduced into the pipe system for mixing with the cheese milk by means of a worm metering device, from which the atmospheric air has been removed by flushing with gaseous carbon dioxide,
EXAMPLE 5
The procedure described in example 1 is repeated ith the change that the starting material is skim milk hich is subjected to diafiltration.
The cheese product obtained is of the same type as a co tage cheese . EXAMP L E 6
Milk with a pH of about 6.5- and about 12% solids, about 3.4?ό protein and about 3.5?ό fat is heated to about 98°C for 15 seconds. Then it is cooled to about 60°C and homogenized at a pressure of about 190 kg/cm2, cooled to about 55°C and ultrafiltrated to provide a retentate with about 38?ό solids.
The retentate is homogenized at about 60 kg/cm2 and is heated to 90°C for about 15 seconds and cooled to about 28°C. Salt in a dry state is mixed with the retentate, and 40 parts of water, 1/2 part of rennet and 20 parts of glucono-delta-lactone are added to the retentate.
The mixture is immediately dispensed in a liquid form into individual packages which are closed hermetically. The packaged product is left to stand until renneting, acidification and coagulation is completed, and is then left for curing at about 5°C.
The produced cheese is of the Feta type and has the composition:
Component Content in g Content in g per Method of per kg of cheese kg of solids analysis
Water/solids 625/375 0/1000 A0AC
Fat 160 427 A0AC
Protein (Nx6.37) 119 317 AACC
Salt 36.9 98.4 A0AC
Glucono-delta- lactone (GDL) 20, 54.4 SLT
Ashes (excl. salt) 9 24.5 A0AC
Phosphor 2.4 6.4 NMK
Carbohydrate 29 77
- ϋ nΛ OA-PI

Claims

P a t e n t C 1 a i m s
1. A process for making portioned cheese, wherein concentrated cheese milk is mixed, preferably continuous- ly, ith ordinary auxiliary substances and additives, including acidogen, for starting the curdling and ripening processes, and then the mixture is filled into individual packages which are closed hermetically and left to stand at a suitable temperature until the curdling and ripening processes are completed, c h a r a c t e r i z e d by using a chemically well-defined acidogen, adapting the amount of the acidogen and the mixing conditions, in¬ cluding temperatures and flow periods, etc., so that the concentrated cheese milk containing the said auxiliary substances and additives coagulate preferably after the introduction into the individual packages and is trans¬ formed through the curdling and ripening processes.
2. A process according to claim 1, c h a r a c t e r - i z e d in that the chemically well-defined acidogen is glucono-delta-lactone.
3. A process according to claim 1 or 2, c h a r a c ¬ t e r i z e d by using a concentrated cheese milk produced by ultrafiItration or diafiltration of milk or skim milk.
4. A process according to claims 1-3, c h a r a c t e r ¬ i z e d by pumping the concentrated cheese milk con¬ tinuously through a closed pipe system, and introducing the additives, including the acidogen, continuously by metering means into the pipe system for mixing with the cheese milk.
5. A process according to claim 4, c h a r a c t e r - i z e d by introducing the acidogen and the other additives into the concentrated cheese milk in the form of an aqueous suspension.
O PI V.ιi-0
6. A process according to claim 4, c h a r a c t e r ¬ i z e d by introducing the acidogen and the other additives into the concentrated cheese milk in the pipe system in the form of a dry powder.
7. A process according to claim 5 or 6, c h a r a c ¬ t e r i z e d by introducing the acidogen into the con¬ centrated cheese milk in the pipe system by means of a worm metering device, from which the atmospheric air has been expelled by means of gaseous carbon dioxide, and further processing the concentrate mixed with the acidogen in the pipe system until it is dispensed directly into the individual packages.
PCT/DK1984/000071 1983-07-28 1984-07-26 A process for making portioned cheese WO1985000501A1 (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
UA3882451A UA5549A1 (en) 1983-07-28 1984-07-26 Method for making cheese
DE8484902915T DE3475259D1 (en) 1983-07-28 1984-07-26 A process for making portioned cheese
AT84902915T ATE38761T1 (en) 1983-07-28 1984-07-26 METHOD OF MAKING CHEESE IN PORTIONS.
FI851232A FI82880C (en) 1983-07-28 1985-03-27 Process for making portion cheese
LV930966A LV5363A3 (en) 1983-07-28 1993-06-30 Saturation of cheese
MD94-0144A MD100C2 (en) 1983-07-28 1994-04-18 Method of pressed cheese obtaining

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DK3460/83A DK346083D0 (en) 1983-07-28 1983-07-28 PROCEDURE FOR MAKING PORTION CHEESE
DK3460/83 1983-07-28

Publications (1)

Publication Number Publication Date
WO1985000501A1 true WO1985000501A1 (en) 1985-02-14

Family

ID=8123122

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/DK1984/000071 WO1985000501A1 (en) 1983-07-28 1984-07-26 A process for making portioned cheese

Country Status (9)

Country Link
US (1) US4716043A (en)
EP (1) EP0149671B1 (en)
AU (1) AU566837B2 (en)
DE (1) DE3475259D1 (en)
DK (1) DK346083D0 (en)
FI (1) FI82880C (en)
SU (1) SU1667620A3 (en)
UA (1) UA5549A1 (en)
WO (1) WO1985000501A1 (en)

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FR2632493A1 (en) * 1988-06-14 1989-12-15 Roquette Freres PROCESS FOR PROVIDING CHEMICAL ABILITIES TO OVERHEATED MILK FOR THE PRODUCTION OF CHEESE EMPRESURES
GR900100536A (en) * 1989-07-13 1991-12-10 Md Foods Amba Method for the continuous production of village type cheese from ultra-filtrated milk
EP0484727A1 (en) * 1990-11-07 1992-05-13 Tetra Laval Holdings & Finance SA Method of producing a cheese and preparing it for distribution
EP0484728A1 (en) * 1990-11-07 1992-05-13 Tetra Laval Holdings & Finance SA Method of producing a cheese and preparing it for distribution
WO1993020704A1 (en) * 1992-04-10 1993-10-28 Ørum Sogns Udviklingsmejeri Method of producing cheese
WO1994024881A1 (en) * 1993-04-27 1994-11-10 Unilever N.V. Fresh, renneted cast cheese and a method of manufacturing
WO1995009537A1 (en) * 1993-10-01 1995-04-13 Tetra Laval Holdings & Finance S.A. A method of producing ready-to-distribute soft/hard cheese
DK178034B1 (en) * 2014-01-24 2015-03-30 Jh Consulting V Jørgen Henriksen Production of acidified white cheese

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SE509182C2 (en) 1992-04-29 1998-12-14 Tetra Laval Holdings & Finance Ways to make and package a cheese-like product
RU2346450C1 (en) * 2007-06-13 2009-02-20 Государственное научное учреждение СИБИРСКИЙ НАУЧНО-ИССЛЕДОВАТЕЛЬСКИЙ ИНСТИТУТ СЫРОДЕЛИЯ Сибирского отделения Российской Академии сельскохозяйственных наук (ГНУ СибНИИС СО РАСХН) Cheese preparation method
FR2933272B1 (en) * 2008-07-04 2014-11-07 Claude Dumarche PROCESS FOR THE PREPARATION OF A LEAVEN FROM RAW MILK, LEAVEN OBTAINED BY THIS PROCESS AND USE OF THE SAME FOR MANUFACTURING A MILK PRODUCT
RU2445778C1 (en) * 2010-08-20 2012-03-27 Открытое акционерное общество "Вимм-Билль-Данн" Cheese preparation method
RU2537269C2 (en) * 2013-02-05 2014-12-27 Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Воронежский государственный аграрный университет имени императора Петра 1" (ФГБОУ ВПО Воронежский ГАУ) Curd product production method

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Cited By (15)

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FR2632493A1 (en) * 1988-06-14 1989-12-15 Roquette Freres PROCESS FOR PROVIDING CHEMICAL ABILITIES TO OVERHEATED MILK FOR THE PRODUCTION OF CHEESE EMPRESURES
US5009914A (en) * 1988-06-14 1991-04-23 Roquette Freres Process for conferring cheese making properties on overheated milks for the manufacture of renneted cheeses
GR900100536A (en) * 1989-07-13 1991-12-10 Md Foods Amba Method for the continuous production of village type cheese from ultra-filtrated milk
WO1992008365A1 (en) * 1990-11-07 1992-05-29 Tetra Pak Holdings S.A. Method of producing a cheese and preparing it for distribution
EP0484728A1 (en) * 1990-11-07 1992-05-13 Tetra Laval Holdings & Finance SA Method of producing a cheese and preparing it for distribution
WO1992008364A1 (en) * 1990-11-07 1992-05-29 Tetra Pak Holdings S.A. Method of producing a cheese and preparing it for distribution
EP0484727A1 (en) * 1990-11-07 1992-05-13 Tetra Laval Holdings & Finance SA Method of producing a cheese and preparing it for distribution
US5232720A (en) * 1990-11-07 1993-08-03 Tetra Alfa Holdings S.A. Method of producing a cheese and preparing it for distribution
US5635228A (en) * 1990-11-07 1997-06-03 Tetra Laval Holdings & Finance S.A. Method of producing a cheese and preparing it for distribution
WO1993020704A1 (en) * 1992-04-10 1993-10-28 Ørum Sogns Udviklingsmejeri Method of producing cheese
WO1994024881A1 (en) * 1993-04-27 1994-11-10 Unilever N.V. Fresh, renneted cast cheese and a method of manufacturing
US5766656A (en) * 1993-04-27 1998-06-16 Unilever Patent Holdings B.V. Fresh, renneted cast cheese and a method of manufacturing
WO1995009537A1 (en) * 1993-10-01 1995-04-13 Tetra Laval Holdings & Finance S.A. A method of producing ready-to-distribute soft/hard cheese
DK178034B1 (en) * 2014-01-24 2015-03-30 Jh Consulting V Jørgen Henriksen Production of acidified white cheese
WO2015110123A1 (en) * 2014-01-24 2015-07-30 Jh Consulting V/Jørgen Henriksen Production of acidified white cheese

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FI82880B (en) 1991-01-31
FI851232A0 (en) 1985-03-27
DE3475259D1 (en) 1988-12-29
EP0149671A1 (en) 1985-07-31
US4716043A (en) 1987-12-29
FI851232L (en) 1985-03-27
FI82880C (en) 1991-05-10
UA5549A1 (en) 1994-12-28
DK346083D0 (en) 1983-07-28
EP0149671B1 (en) 1988-11-23
SU1667620A3 (en) 1991-07-30
AU3217584A (en) 1985-03-04
AU566837B2 (en) 1987-10-29

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